Gadalla Mamdouh A, Olujic Zarko, Jansens Peter J, Jobson Megan, Smith Robin
Laboratory for Process Equipment, TU Delft, Leeghwaterstraat 44, 2628 CA Delft, The Netherlands.
Environ Sci Technol. 2005 Sep 1;39(17):6860-70. doi: 10.1021/es049795q.
Distillation systems are energy and power intensive processes and contribute significantly to the greenhouse gases emissions (e.g. carbon dioxide). Reducing CO2 emissions is an absolute necessity and expensive challenge to the chemical process industries in orderto meetthe environmental targets as agreed in the Kyoto Protocol. A simple model for the calculation of CO2 emissions from heat-integrated distillation systems is introduced, considering typical process industry utility devices such as boilers, furnaces, and turbines. Furnaces and turbines consume large quantities of fuels to provide electricity and process heats. As a result, they produce considerable amounts of CO2 gas to the atmosphere. Boilers are necessary to supply steam for heating purposes; besides, they are also significant emissions contributors. The model is used in an optimization-based approach to optimize the process conditions of an existing crude oil atmospheric tower in order to reduce its CO2 emissions and energy demands. It is also applied to generate design options to reduce the emissions from a novel internally heat-integrated distillation column (HIDiC). A gas turbine can be integrated with these distillation systems for larger emissions reduction and further energy savings. Results show that existing crude oil installations can save up to 21% in energy and 22% in emissions, when the process conditions are optimized. Additionally, by integrating a gas turbine, the total emissions can be reduced further by 48%. Internal heat-integrated columns can be a good alternative to conventional heat pump and other energy intensive close boiling mixtures separations. Energy savings can reach up to 100% with respect to reboiler heat requirements. Emissions of these configurations are cut down by up to 83%, compared to conventional units, and by 36%, with respect to heat pump alternatives. Importantly, cost savings and more profit are gained in parallel to emissions minimization.
蒸馏系统是能源和电力密集型工艺,对温室气体排放(如二氧化碳)有重大贡献。减少二氧化碳排放对化工行业来说是绝对必要且代价高昂的挑战,以便实现《京都议定书》中商定的环境目标。本文介绍了一种用于计算热集成蒸馏系统二氧化碳排放的简单模型,该模型考虑了典型的过程工业公用设备,如锅炉、熔炉和涡轮机。熔炉和涡轮机消耗大量燃料来提供电力和工艺热。因此,它们会向大气中排放大量的二氧化碳气体。锅炉是提供加热用蒸汽所必需的;此外,它们也是重要的排放源。该模型用于基于优化的方法来优化现有原油常压塔的工艺条件,以减少其二氧化碳排放和能源需求。它还被应用于生成设计方案,以减少新型内部热集成蒸馏塔(HIDiC)的排放。燃气轮机可与这些蒸馏系统集成,以实现更大程度的减排和进一步的节能。结果表明,优化工艺条件后,现有原油装置可节能21%,减排22%。此外,通过集成燃气轮机,总排放量可进一步降低48%。内部热集成塔可以是传统热泵和其他能源密集型近沸混合物分离的良好替代方案。相对于再沸器热需求,节能可达100%。与传统装置相比,这些配置的排放量最多可减少83%,与热泵替代方案相比可减少36%。重要的是,在实现排放最小化的同时还能节省成本并获得更多利润。